FI842924A0 - KONTINUERLIGT ARBETANDE VAERMEVAEXLARE. - Google Patents
KONTINUERLIGT ARBETANDE VAERMEVAEXLARE.Info
- Publication number
- FI842924A0 FI842924A0 FI842924A FI842924A FI842924A0 FI 842924 A0 FI842924 A0 FI 842924A0 FI 842924 A FI842924 A FI 842924A FI 842924 A FI842924 A FI 842924A FI 842924 A0 FI842924 A0 FI 842924A0
- Authority
- FI
- Finland
- Prior art keywords
- lower chamber
- tubes
- return tube
- jacket
- pressure difference
- Prior art date
Links
- 239000012530 fluid Substances 0.000 abstract 2
- 238000001311 chemical methods and process Methods 0.000 abstract 1
- 239000008187 granular material Substances 0.000 abstract 1
- 239000000463 material Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
- B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
- B01J8/386—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only internally, i.e. the particles rotate within the vessel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D13/00—Heat-exchange apparatus using a fluidised bed
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/008—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using scrapers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28G—CLEANING OF INTERNAL OR EXTERNAL SURFACES OF HEAT-EXCHANGE OR HEAT-TRANSFER CONDUITS, e.g. WATER TUBES OR BOILERS
- F28G9/00—Cleaning by flushing or washing, e.g. with chemical solvents
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/0091—Powders
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- Medicinal Chemistry (AREA)
- Analytical Chemistry (AREA)
- Food Science & Technology (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
- Steroid Compounds (AREA)
- Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)
- Detergent Compositions (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- External Artificial Organs (AREA)
- Non-Silver Salt Photosensitive Materials And Non-Silver Salt Photography (AREA)
- Thermotherapy And Cooling Therapy Devices (AREA)
Abstract
This invention relates to apparatus for carrying out physical and/or chemical processes, more specifically a heat exchanger (10) of the continuous type, comprising a large number of vertical heat exchanger tubes (18) mounted between a lower chamber (17) and an upper chamber (16) within a jacket (15). Within the tubes (18) small solid particles are kept in a fluidized condition by the fluid medium passing up from the lower chamber (17) through the tubes (18), so as to achieve a good heat transfer, whereas also any deposit will be removed from the innertube walls. Forthe downward flow of the granular mass at least one return tube (21) is provided. Downward circulation of the fluid medium through the return tube (21) should be minimal, however, which can be achieved by an increase of the pressure difference between the upper and lower chamber (16; 17), which increase of the pressure difference can be achieved by fitting several distribution plates (24; 42) at a level above the return tube (21) outlet into the lower chamber (17), preferably so thatthe apertures in the various distribution plates (24; 42) of the multiple design are not vertically in line.The second distribution plate (42) also serves to minimise excessive wear of the material of the jacket (15) due to the eddying motion of the granules.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI885140A FI885140A0 (en) | 1983-07-22 | 1988-11-08 | ANORDNING FOER GENOMFOERANDE AV PHYSIKALISKA OCH / ELLER KEMISKA PROCESSER, I SYNNERHET KONTINUERLIGT ARBETANDE VAERMEVAEXLARE. |
FI885139A FI86916C (en) | 1983-07-22 | 1988-11-08 | ANORDINATION FOR GENERIC OPERATION OF PHYSICAL OCH / ELLER CHEMICAL PROCESSER, I SYNNERHET KONTINUERLIGT ARBETANDE VAERMEVAEXLARE |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL8302622 | 1983-07-22 | ||
NL8302622A NL192055C (en) | 1983-07-22 | 1983-07-22 | Device for operating physical and / or chemical processes, in particular a heat exchanger with circulation of granular mass. |
Publications (4)
Publication Number | Publication Date |
---|---|
FI842924A0 true FI842924A0 (en) | 1984-07-20 |
FI842924A FI842924A (en) | 1985-01-23 |
FI77528B FI77528B (en) | 1988-11-30 |
FI77528C FI77528C (en) | 1989-03-10 |
Family
ID=19842192
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FI842924A FI77528C (en) | 1983-07-22 | 1984-07-20 | ANORDNING ATT GENOMFOERA PHYSICAL OCH / ELLER CHEMICAL PROCESSER, I SYNNERHET EN KONTINUERLIGT ARBETANDE VAERMEVAEXLARE. |
Country Status (15)
Country | Link |
---|---|
US (3) | US4567940A (en) |
EP (3) | EP0228143B1 (en) |
JP (1) | JPS6089686A (en) |
KR (1) | KR910002109B1 (en) |
AT (2) | ATE41227T1 (en) |
AU (1) | AU561787B2 (en) |
BR (1) | BR8403638A (en) |
CA (1) | CA1232602A (en) |
DE (1) | DE3466062D1 (en) |
DK (1) | DK162123C (en) |
ES (3) | ES534495A0 (en) |
FI (1) | FI77528C (en) |
IN (1) | IN161954B (en) |
NL (2) | NL192055C (en) |
NO (1) | NO163650C (en) |
Families Citing this family (38)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3432864A1 (en) * | 1984-09-07 | 1986-03-20 | Robert Prof. Dr.-Ing. 5100 Aachen Rautenbach | Heat exchanger for the physical and/or chemical treatment of a liquid |
US4665632A (en) * | 1985-09-27 | 1987-05-19 | Uop Inc. | Apparatus for uniformly distributing fluid through a bed of particulate material |
US4662081A (en) * | 1985-09-27 | 1987-05-05 | Uop Inc. | Process for uniformly distributing fluid through a bed of particulate material |
NL192750C (en) * | 1986-09-30 | 1998-01-06 | Eskla Bv | Device for operating physical and / or chemical processes, in particular a heat exchanger. |
US4896704A (en) * | 1988-01-27 | 1990-01-30 | Mobil Oil Corp. | Loading techniques for downflow reactors |
US4904452A (en) * | 1988-03-31 | 1990-02-27 | Union Carbide Chemicals And Plastics Company Inc. | Inner core heating in fluidized bed |
DE3818819C2 (en) * | 1988-06-03 | 1997-09-25 | Sgl Technik Gmbh | Heat transfer device |
DE3831385C2 (en) * | 1988-09-15 | 1997-06-12 | Sgl Technik Gmbh | Method and device for operating a tube bundle apparatus |
DE3939029A1 (en) * | 1989-11-25 | 1991-05-29 | Rautenbach Robert | Fluidised red heat exchanger - has material of fluidised bed stored in gas inlet chamber at beginning of operation |
DE4102118A1 (en) * | 1991-01-25 | 1992-07-30 | Jochen Stephan Dipl I Kollbach | HEAT EXCHANGER WITH CIRCULATING FLUID BED |
US5141047A (en) * | 1991-03-01 | 1992-08-25 | Riley Stoker Corporation | Fluidized bed heat exchanger |
US10361802B1 (en) | 1999-02-01 | 2019-07-23 | Blanding Hovenweep, Llc | Adaptive pattern recognition based control system and method |
US8352400B2 (en) | 1991-12-23 | 2013-01-08 | Hoffberg Steven M | Adaptive pattern recognition based controller apparatus and method and human-factored interface therefore |
NL9300666A (en) * | 1993-04-20 | 1994-11-16 | Bronswerk Heat Transfer Bv | Device for carrying out a physical and / or chemical process, such as a heat exchanger. |
US5798137A (en) | 1995-06-07 | 1998-08-25 | Advanced Silicon Materials, Inc. | Method for silicon deposition |
NL1005514C2 (en) * | 1997-03-12 | 1998-09-15 | Bronswerk Heat Transfer Bv | Device for carrying out a physical and / or chemical process, such as a heat exchanger. |
NL1005518C2 (en) * | 1997-03-12 | 1998-09-15 | Bronswerk Heat Transfer Bv | Device for carrying out a physical and / or chemical process, such as a heat exchanger. |
NL1005517C2 (en) * | 1997-03-12 | 1998-09-15 | Bronswerk Heat Transfer Bv | Device for carrying out a physical and / or chemical process, such as a heat exchanger. |
US7904187B2 (en) | 1999-02-01 | 2011-03-08 | Hoffberg Steven M | Internet appliance system and method |
US6262190B1 (en) | 1999-02-10 | 2001-07-17 | Union Carbide Chemicals & Plastics Technology Corporation | Process and apparatus for fluid bed polymerization |
US6698501B2 (en) * | 2001-07-25 | 2004-03-02 | William H. Fleischman | Heat exchangers that contain and utilize fluidized small solid particles |
US7575043B2 (en) * | 2002-04-29 | 2009-08-18 | Kauppila Richard W | Cooling arrangement for conveyors and other applications |
KR100482827B1 (en) * | 2002-09-14 | 2005-04-14 | 삼성전자주식회사 | Heat exchanger |
CN100354593C (en) * | 2003-06-13 | 2007-12-12 | 株洲工学院帅科机械清洗研究所 | Horizontal column type heat exchanger exterior dirt three-phase fluidization in-situ cleaning process |
CN1657860B (en) * | 2004-02-16 | 2010-05-12 | 湖南工业大学 | Vertical tubulation heat-transfer equipment with on-line fluidization cleaning function for dirt on outer of pipe |
MXPA06003045A (en) * | 2006-03-17 | 2007-09-17 | Mexicano Inst Petrol | Improved equipment for the exchange of heat between liquids and fluids. |
JP5308795B2 (en) * | 2007-12-11 | 2013-10-09 | 住友化学株式会社 | Polyolefin production method and polyolefin production system provided with spouted bed apparatus |
JP5427396B2 (en) * | 2007-12-11 | 2014-02-26 | 住友化学株式会社 | Powder transfer apparatus and polyolefin production method |
JP5308794B2 (en) * | 2007-12-11 | 2013-10-09 | 住友化学株式会社 | Polyolefin production method using spouted bed apparatus |
JP5308797B2 (en) * | 2007-12-11 | 2013-10-09 | 住友化学株式会社 | Olefin polymerization reaction apparatus, polyolefin production system, and polyolefin production method |
JP5249730B2 (en) * | 2007-12-11 | 2013-07-31 | 住友化学株式会社 | Olefin polymerization reaction apparatus and polyolefin production method |
JP5545800B2 (en) * | 2009-06-08 | 2014-07-09 | 住友化学株式会社 | Jet-fluidized bed type olefin polymerization reactor, polyolefin production system, and polyolefin production method |
CN103101989B (en) * | 2013-02-05 | 2014-07-30 | 双良节能系统股份有限公司 | Self-cleaning high-salt wastewater evaporative crystallization device |
US20160341499A1 (en) * | 2015-05-19 | 2016-11-24 | Uop Llc | Process for online cleaning of mto reactor effluent cooler |
JP6902337B2 (en) | 2016-08-03 | 2021-07-14 | 住友化学株式会社 | Method for producing heterophasic propylene polymerized material |
JP6938421B2 (en) * | 2018-04-17 | 2021-09-22 | 株式会社神戸製鋼所 | Fluid flow device |
CN109045947B (en) * | 2018-09-03 | 2021-08-17 | 青岛科技大学 | Fluidized bed cluster reactor |
CN109499262B (en) * | 2018-12-14 | 2021-08-13 | 青岛科技大学 | Novel longitudinal parallel bed adsorber |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2488406A (en) * | 1947-11-25 | 1949-11-15 | Gulf Research Development Co | Method and apparatus for conducting chemical reactions |
US2559069A (en) * | 1949-07-30 | 1951-07-03 | Standard Oil Co | Choke for abrasive fluids |
US2591595A (en) * | 1949-09-29 | 1952-04-01 | Standard Oil Dev Co | Method for controlling the temperature of exothermic reactions such as the gasification of carbonaceous solids |
US3055745A (en) * | 1952-11-07 | 1962-09-25 | Vulcan Cincinnati Inc | Catalytic reactor |
US2884373A (en) * | 1954-10-20 | 1959-04-28 | Exxon Research Engineering Co | Method and apparatus for heating fluids |
FR1183779A (en) * | 1956-10-29 | 1959-07-13 | Dorr Oliver Inc | Heat recovery in a fluidized solids process |
US3476655A (en) * | 1967-11-01 | 1969-11-04 | Us Interior | Descaling of saline water and distillation |
GB1326651A (en) * | 1971-01-29 | 1973-08-15 | Coal Industry Patents Ltd | Method and apparatus for the generation and transfer of heat in fluidised bed systems |
US4300625A (en) * | 1975-01-21 | 1981-11-17 | Mikhailov Gerold M | Preventing deposition on the inner surfaces of heat exchange apparatus |
NL170458C (en) * | 1975-05-20 | 1982-11-01 | Ir Gustav Adolf Pieper | HEAT EXCHANGER, INCLUDING A GRANULATIC CONTAINER CONTAINING VERTICAL TUBES, AND METHOD FOR ITS COMPANY. |
NL7703939A (en) * | 1977-04-12 | 1978-10-16 | Esmil Bv | METHOD AND APPARATUS FOR HEAT EXCHANGE |
US4142578A (en) * | 1977-09-12 | 1979-03-06 | Exxon Research & Engineering Co. | Heat exchanger impingement protection |
NL181753C (en) * | 1978-02-16 | 1987-10-16 | Esmil Bv | Apparatus for operating physical and / or chemical processes comprising a bundle of parallel and vertically arranged pipes. |
NL184024C (en) * | 1980-09-05 | 1989-03-16 | Esmil Bv | DEVICE WITH A NUMBER OF HEAT EXCHANGERS PLACED ABOVE EACH OTHER. |
NL187770C (en) * | 1980-11-12 | 1992-01-02 | Esmil Bv | FLOW-UP DEVICE FOR A LIQUID MEDIUM CONTAINING A FLUIDISABLE GRAIN MASS. |
GB2087532A (en) * | 1980-11-18 | 1982-05-26 | British Steam Specialties The | Heat exchangers |
NL8102308A (en) * | 1981-05-12 | 1982-12-01 | Esmil Bv | DEVICE FOR OPERATING PHYSICAL AND / OR CHEMICAL PROCESSES, IN PARTICULAR A HEAT EXCHANGER. |
NL8102307A (en) * | 1981-05-12 | 1982-12-01 | Esmil Bv | Apparatus and method for thickening by evaporation of a liquid. |
GB2105455A (en) * | 1981-09-09 | 1983-03-23 | Vyzk Ustav Chem Zarizeni | An apparatus for indirect cooling of fluids by a gas stream |
-
1983
- 1983-07-22 NL NL8302622A patent/NL192055C/en not_active IP Right Cessation
-
1984
- 1984-07-09 DE DE8484200984T patent/DE3466062D1/en not_active Expired
- 1984-07-09 AT AT86202384T patent/ATE41227T1/en not_active IP Right Cessation
- 1984-07-09 EP EP86202384A patent/EP0228143B1/en not_active Expired
- 1984-07-09 AT AT86202385T patent/ATE39384T1/en active
- 1984-07-09 EP EP86202385A patent/EP0228144B1/en not_active Expired
- 1984-07-09 EP EP84200984A patent/EP0132873B1/en not_active Expired
- 1984-07-11 AU AU30492/84A patent/AU561787B2/en not_active Ceased
- 1984-07-11 US US06/629,810 patent/US4567940A/en not_active Expired - Lifetime
- 1984-07-16 CA CA000458992A patent/CA1232602A/en not_active Expired
- 1984-07-18 DK DK351584A patent/DK162123C/en not_active IP Right Cessation
- 1984-07-18 IN IN518/MAS/84A patent/IN161954B/en unknown
- 1984-07-20 FI FI842924A patent/FI77528C/en not_active IP Right Cessation
- 1984-07-20 NO NO842970A patent/NO163650C/en unknown
- 1984-07-20 BR BR8403638A patent/BR8403638A/en not_active IP Right Cessation
- 1984-07-20 ES ES534495A patent/ES534495A0/en active Granted
- 1984-07-21 KR KR1019840004345A patent/KR910002109B1/en not_active IP Right Cessation
- 1984-07-21 JP JP59150512A patent/JPS6089686A/en active Granted
-
1985
- 1985-06-01 ES ES543812A patent/ES8703619A1/en not_active Expired
- 1985-10-04 US US06/783,956 patent/US4615382A/en not_active Expired - Fee Related
-
1986
- 1986-01-15 US US06/819,297 patent/US4640339A/en not_active Expired - Fee Related
- 1986-07-30 ES ES556983A patent/ES8707604A1/en not_active Expired
-
1993
- 1993-12-02 NL NL9302096A patent/NL9302096A/en not_active Application Discontinuation
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM | Patent lapsed | ||
MM | Patent lapsed |
Owner name: ESKLA B.V. |